EP3868472B1 - Antifouling oligomerization catalyst systems - Google Patents

Antifouling oligomerization catalyst systems Download PDF

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Publication number
EP3868472B1
EP3868472B1 EP21155202.1A EP21155202A EP3868472B1 EP 3868472 B1 EP3868472 B1 EP 3868472B1 EP 21155202 A EP21155202 A EP 21155202A EP 3868472 B1 EP3868472 B1 EP 3868472B1
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catalyst system
titanate
antifouling
compound
total
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English (en)
French (fr)
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EP3868472A2 (en
EP3868472A3 (en
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Sohel Shaikh
Motaz KHAWAJI
Hussain AL YAMI
Wei Xu
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Saudi Arabian Oil Co
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Saudi Arabian Oil Co
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Priority to EP23186812.6A priority Critical patent/EP4257234B1/en
Priority to EP25168237.3A priority patent/EP4582181A1/en
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    • B01J31/00—Catalysts comprising hydrides, coordination complexes or organic compounds
    • B01J31/02—Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides
    • B01J31/06—Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides containing polymers
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    • B01J31/0234—Nitrogen-, phosphorus-, arsenic- or antimony-containing compounds
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    • C07C2/00—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms
    • C07C2/02—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms by addition between unsaturated hydrocarbons
    • C07C2/04—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms by addition between unsaturated hydrocarbons by oligomerisation of well-defined unsaturated hydrocarbons without ring formation
    • C07C2/06—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms by addition between unsaturated hydrocarbons by oligomerisation of well-defined unsaturated hydrocarbons without ring formation of alkenes, i.e. acyclic hydrocarbons having only one carbon-to-carbon double bond
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    • B01J2231/20—Olefin oligomerisation or telomerisation
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    • C07C2531/26—Catalysts comprising hydrides, coordination complexes or organic compounds containing in addition, inorganic metal compounds not provided for in groups C07C2531/02 - C07C2531/24
    • C07C2531/38—Catalysts comprising hydrides, coordination complexes or organic compounds containing in addition, inorganic metal compounds not provided for in groups C07C2531/02 - C07C2531/24 of titanium, zirconium or hafnium

Definitions

  • Embodiments of the present disclosure generally relate to catalyst systems used in ethylene oligomerization, and more specifically relate to antifouling catalyst systems used in ethylene oligomerization which may reduce undesired polymerization.
  • 1-Butene and 1-hexene are important petrochemicals, especially for the production of polyethylene.
  • LLDPE linear low density polyethylene
  • a source of 1-butene is the butene fraction from the effluent of a hydrocarbon cracker, such as a steam cracker or fluidized catalytic cracker.
  • a hydrocarbon cracker such as a steam cracker or fluidized catalytic cracker.
  • the process for recovering 1-butene from such an effluent requires several difficult process steps that may make the process undesirable.
  • a commercially successful dimerization process is the Alphabutol TM Process, developed by the Institute Francais du Petrole (IFP), described in A. Forestiere, et al., "Oligomerization of Monoolefins by Homogenous Catalysts", Oil & Science and Technology-Review de l'Institute Francais du Petrole, pages 663-664 (Volume 64, Number 6, November 2009 ).
  • IFP Institute Francais du Petrole
  • This process uses a bubble-point reactor that contains 1-butene as a process fluid to oligomerize ethylene selectively into 1-butene.
  • a hot spot is an area where external cooling is ineffective and catalyst activity is high. It represents a loss of process control.
  • a hot spot can be an area of collected polymer that includes catalytically active material that fosters side-reactions, including polymerization. If left unchecked, the hot spot can eventually lead to a process shutdown due to the loss of cooling capacity, a runaway polymerization reaction, or both.
  • US5792895 discloses a catalyst system comprising a titanate, an aluminum compound and a polyethylene glycol, or a monoester or a monoether thereof, for the production of 1-butene from ethylene, wherein the polyethylene glycol reduces the adhesion of solid polymer by-products to the walls of the reactor.
  • a catalyst system that may reduce polymeric fouling may comprise at least one titanate compound, at least one aluminum compound, and an antifouling agent.
  • the antifouling agent according to the invention comprises an ester comprising a cyclic moiety, wherein the ester moiety is included in the cyclic moiety.
  • the catalyst system may further comprise a non-polymeric ether compound.
  • 1-butene may be selectively produced by a method that comprises contacting ethylene with a catalyst system to oligomerize the ethylene to selectively form 1-butene.
  • the catalyst system comprises at least one titanate compound, at least one aluminum compound, and an antifouling agent.
  • the antifouling agent comprises an ester comprising a cyclic moiety, wherein the ester moiety is included in the cyclic moiety.
  • One or more embodiments of the present disclosure are directed to catalyst systems which may be utilized in promoting ethylene oligomerization, such as the dimerization of ethylene to form 1-butene or 1-hexene, while reducing reactor fouling caused by undesired polymerization.
  • These catalyst systems are sometimes referred to in this disclosure as “antifouling ethylene oligomerization catalyst systems” or “antifouling catalyst systems”.
  • the antifouling catalyst systems described comprise at least one titanate compound, at least one aluminum compound, and at least one antifouling agent comprising an ester comprising a cyclic moiety, wherein the ester moiety is included in the cyclic moiety.
  • the antifouling catalyst systems may further comprise one or more non-polymeric ether compounds, and the components of the antifouling catalyst system may be mixed in a solvent such as hexane.
  • the antifouling catalyst systems may be used to selectively oligomerize ethylene to produce 1-butene, while reducing undesirable polymerization, sometimes referred to in this disclosure as "fouling".
  • reactor fouling may occur due to the formation of solid polyethylene-based residues which may reduce fluid flow and fully block or at least partially block fluids in a reactor system from flowing at a desired rate. It should be understood that the "antifouling ethylene oligomerization catalyst systems" or “antifouling catalyst systems” described may not completely eliminate fouling during a reaction.
  • catalyst systems reduce fouling as compared with catalyst systems which do not include an antifouling agent as described in the present disclosure.
  • the catalyst systems of the present disclosure may be useful in ethylene oligomerization reactions, such as ethylene dimerization to form 1-butene, they may also be useful for the catalysis of other chemical reactions, and the antifouling catalyst systems described in this disclosure should not be considered limited in their use to the dimerization of ethylene to 1-butene.
  • the antifouling agents described in this disclosure may be incorporated with other catalyst systems which contain, for example, non-titanium based catalysts.
  • embodiments of the described antifouling catalyst systems comprise one or more titanate compounds which may serve as a catalyst in the catalyst systems described in this disclosure. While several titanate compounds may be included in the antifouling catalyst system, in some embodiments a single titanate compound may be included in the antifouling catalyst system.
  • the titanate compound may be an alkyl titanate.
  • An alkyl titanate may have the structure Ti(OR) 4 in which R is a branched or straight chain alkyl group.
  • each alkyl group may comprise from 2 to 8 carbons, where each R group may be the same or different.
  • Suitable alkyl titanates may include tetraethyl titanate, tetraisopropyl titanate, tetra-n-butyl titanate (sometimes referred to as titanium butoxide or tetrabutyl orthotitanate), 2-tetraethylhexyl titanate, or combinations thereof.
  • the titanate compound of the antifouling catalyst system consists of tetra-n-butyl titanate.
  • embodiments of the described antifouling catalyst systems comprise one or more aluminum compounds which may act as co-catalysts in the catalyst systems described in this disclosure. While several aluminum compounds may be included in the antifouling catalyst system, in some embodiments a single aluminum compound may be included. In one or more embodiments, one or more aluminum alkyl compounds may be included in the antifouling catalyst system.
  • Aluminum alkyl compounds may have a structure of AlR' 3 or AlR' 2 H, where R' is a straight chain or branched alkane comprising from 1 to 20 carbons, or an aluminoxane structure (that is, a partial hydrolysate of trialkylaluminum compounds).
  • the R' groups of the aluminum alkyl compounds may be the same or different from one another.
  • suitable aluminum alkyl compounds may include triethylaluminum, tripropylaluminum, tri-iso-butylaluminum, trihexylaluminum, or combinations thereof.
  • the aluminum compound of the antifouling catalyst system consists of triethylaluminum.
  • the antifouling catalyst systems described in this disclosure include at least one antifouling agent.
  • the antifouling agent comprises an ester comprising a cyclic moiety, wherein the ester moiety is included in the cyclic moiety.
  • An antifouling agent is an additive to a catalyst system which decreases fouling by polymer production.
  • the antifouling agent comprises an ester comprising a cyclic moiety, wherein the ester moiety is included in the cyclic moiety.
  • Suitable ester antifouling agents include, without limitation, ⁇ -caprolactone.
  • antifouling agent that is a single chemical species
  • two or more different antifouling agent species may be present as the antifouling agent.
  • two or more different antifouling agent species of the same type may be present.
  • the catalyst system may comprise two different species of esters.
  • the antifouling catalyst system may comprise one or more non-polymeric ether compounds.
  • the one or more ether compounds may include cyclic non-polymeric ethers such as, but not limited to, tetrahydrofuran (THF), a dioxane, a tetrahydropyran (THP), or combinations thereof.
  • non-polymeric ethers refer to compounds which include one or more ethers but do not include long ether polymer chains. Usually, these non-polymeric ethers comprise one or two ether moieties, and comprise less than 10 ether moieties.
  • antifouling catalyst systems which include esters as antifouling agents may be particularly suited for not including an ester. It is believed that the ester functionalities of some antifouling agents may at least partially replicate or mimic the functionality of ethers in the antifouling catalyst systems, rendering some embodiments of antifouling catalyst systems which include esters sufficient for their purpose without an additional ether compound.
  • the antifouling catalyst systems may comprise at least one or more titanate compounds, one or more aluminum compounds, and one or more antifouling agents.
  • the molar ratio of total titanate compound to total aluminum compound may be from 1:10 to 1:1 (such as, for example, from 1:10 to 1:2, from 1:10 to 1:3, from 1:10 to 1:4, from 1:10 to 1:5, from 1:10 to 1:6, from 1:10 to 1:7, from 1:10 to 1:8, from 1:10 to 1:9, from 1:9 to 1:1, from 1:8 to 1:1, from 1:7 to 1:1, from 1:6 to 1:1, from 1:5 to 1:1, from 1:4 to 1:1, from 1:3 to 1:1, or from 1:2 to 1).
  • the molar ratio of total titanate compounds to total antifouling agent may be from 1:10 to 1:0.01 (such as, for example, from 1:10 to 1:0.05, from 1:10 to 1:0.1, from 1:10 to 1:0.3, from 1:10 to 1:0.5, from 1:10 to 1:0.7, from 1:10 to 1:1, from 1:10 to 1:2, from 1:10 to 1:3, from 1:10 to 1:5, from 1:5 to 1:0.01, from 1:3 to 1:0.01, from 1:2 to 1:0.01, from 1:1 to 1:0.01, from 1:0.7 to 1:0.01, or from 1:0.3 to 1:0.01).
  • 1:10 to 1:0.01 such as, for example, from 1:10 to 1:0.05, from 1:10 to 1:0.1, from 1:10 to 1:0.3, from 1:10 to 1:0.5, from 1:10 to 1:0.7, from 1:10 to 1:1, from 1:10 to 1:2, from 1:10 to 1:3, from 1:10 to 1:5, from 1:5 to 1:0.01, from 1:3 to 1:0.01, from 1:2 to 1
  • the molar ratio of total titanate compounds to total non-polymeric ether compounds may be from 1:10 to 1:0 (such as, for example, from 1:5 to 1:0, from 1:3 to 1:0, from 1:2 to 1:0, from 1:1 to 1:0, from 1:0.5 to 1:0, from 1:0.3 to 1:0, from 1:0.1 to 1:0, from 1:10 to 1:0.1, from 1:10 to 1:0.5, from 1:10 to 1:1, from 1:10 to 1:2, or from 1:10 to 1:5).
  • the molar ratios of components of the antifouling catalyst systems described previously in this disclosure are representative of the total amount of each component of the antifouling catalyst system relative to the total amount of titanate compound, where the "total" amount refers to the molar amount of all species of the antifouling catalyst system which may be considered as a particular component type (that is, titanate compound, aluminum compound, non-polymeric ether compound, or antifouling agent).
  • the total amount of a component may include two or more chemical species which are titanate compounds, aluminum compounds, non-polymeric ether compounds, or antifouling agents, respectively.
  • 1-butene may be produced by contacting ethylene with the antifouling catalyst system described previously to oligomerize the ethylene to form 1-butene.
  • the ethylene and antifouling catalyst system are supplied to a reactor and mixed.
  • the reaction may be performed as a batch reaction or as a continuous process reaction, such as a continuous stir tank reactor process.
  • the pressure of the reactor may be from 5 bar to 100 bar, and the reactor temperature may be from 30 degrees Celsius (°C) to 180 °C.
  • process conditions outside of these ranges are contemplated, especially in view of the specific design of the reactor system and concentrations of the reactants and catalysts.
  • the reactions of the present disclosure primarily limit or do not include polymerization of ethylene (for example, polymers comprising 100 or more monomer ethylene units).
  • polymer formation may be limited to less than 500, less than 300, or even less than 100 parts per million of reactant.
  • heteroatoms of the antifouling agents may form weak coordination with the titanate compound utilized as the catalyst in the catalyst system. It is believed that, in one or more embodiments, the alkyl groups or other relatively long-chained groups of the antifouling agents may serve in some capacity to prevent ethylene access to the catalytic center of the titanate compound. The restriction of access of the ethylene to the titanate catalytic site may reduce the polymerization of ethylene and thus reduce reactor fouling.
  • the introduction of the antifouling agent into a catalyst system may suppress polymer formation while not greatly reducing catalytic activity of 1-butene formation.
  • polymer formation may be reduced by at least 5%, 10%, 20%, 30%, 40%, 50%, 60%, 70%, 80%, 90%, or even 95% by the inclusion of an antifouling agent.
  • 1-butene production may be increased, stay the same, or may decrease by less than or equal to 50%, 40%, 30%, 20%, 10% or even 5% by the inclusion of an antifouling agent.
  • antifouling agents may both reduce the polymer formation (such as by at least 5%, 10%, 20%, 30%, 40%, 50%, 60%, 70%, 80%, 90% or even 95%) and increase, not effect, or decrease 1-butene production rate by less than or equal to 50%, 40%, 30%, 20%, 10% or even 5%.
  • Reduction in polymer formation rates and catalytic activity on a percentage basis are based on catalyst systems which include one or more antifouling agents described as compared with catalyst systems which are void of an antifouling agent.
  • Example #14 is an example according to the present invention, and Examples #1 - #13 are reference examples.
  • catalyst mixtures were used that contained titanium tetrabutoxide (denoted as “Ti” in Table 1), THF, triethyl aluminum (sometimes referred to as “TEAL”), and antifouling agents (denoted as "AFA” in Table 1).
  • Ti titanium tetrabutoxide
  • THF triethyl aluminum
  • AFA antifouling agents
  • the molar ratio of Ti:AFA for each example is listed in Table 1.
  • the molar ratio of Ti:THF:TEAL in the examples was 1:6:7.5.
  • the oligomerization experiments were conducted in a rig which included 8 autoclave reactors each having a volume of 400 milliliters (mL). Prior to the experimental runs, the rig was subjected to inertization process which included evacuating the reactors with an oil vacuum pump and heating to 160 °C.
  • the rig was pressurized to 4 bar with nitrogen and the stirrers were operated with a stirring speed of about 300 rpm. Then, three minutes following the start of the pressurization, the gas outlet valves were opened to release the nitrogen to the exhaust. Two minutes after the gas release had started, the valves from the main exhaust pipe to the vacuum pump were opened to evacuate the rig. The rig was evacuated for 15 minutes. The gas outlet valves were then closed, and the rig was pressurized with nitrogen again. The pump-pressurize cycles were run for at least 30 hours. The rig was then evacuated in vacuum for a further 6 to 8 hours. During the last one hour, the autoclave reactors were cooled down to 45 °C. The rig was then pressurized to 3 bar until the reaction was started.
  • Chargers were prepared, which included the components of the catalyst mixtures.
  • two stock solutions were prepared in a glove box. Heptane was utilized as a solvent, and an amount of heptane was utilized, such that the autoclave reactors were nominally filled.
  • the first solution contained the TEAL co-catalyst mixed with 90% of the heptane.
  • the second solution contained the titanium tetrabutoxide catalyst, the THF, and the antifouling agents mixed with 10% of the heptane.
  • the first solution and the second solution were put into first solution chargers and second solution chargers, respectively.
  • the pressure in the rig was released to about 0.2 bar.
  • the chargers with the second solution of TEAL/heptane were injected into the reactors.
  • the charging was achieved by pressurizing the chargers with ethylene to 10 bar and opening the valve between the charger and the reactor.
  • the contents of the second solution charger were then injected, using ethene as the charging gas with a pressure of 35 bar.
  • the target pressure for the reactors was set to 23 bar.
  • the gas dosage into the reactor was started automatically.
  • the temperature in the reactor rose and the temperature was set to the target value of 53.5 °C. After the start of the ethene dosage, the reaction was run for 75 min.
  • the reaction was terminated by the injection of 1 mL of ethanol.
  • the pressure was released from the reactors, and the temperature was set to 20 °C.
  • the reactors were opened and the contents of the reactor, including the baffles and stirrers, were removed and placed in a heating oven at 75 °C for one hour.
  • the residue in the reactor was then washed with a 10 wt.% aqueous sulfuric acid solution to dissolve any catalyst residues.
  • the remaining solid polymer was filtered and dried overnight in an oven at 110°C and weighed. Table 1 shows the dimerization activity and weight of polymer deposit for reactions which utilized each of the sample catalyst systems.
  • Example #14 is an example according to the present invention, and Examples #1 - #13 are reference examples.
  • Table 1 Experiment Number Molar Ratio of Ti;AFA Activity (grams of ethylene per hour per millimoles of titanium Polymer Produced in parts per million (and in mg) AFA chemical species Comparative Example 1:0 228 1,310 (149) N/A Example #1 0.3:1 237 55 (6.5) tetrabutylphosphonium bromide Example #2 0.3:1 9 0(0) tetrabutylphosphonium malonate Example #3 0.3:1 216 97 (8) sodium dodecylbenzenesulfonate Example #4 3:1 208 96 (10) sodium dodecylbenzenesulfonate Example #5 0.3:1 166 187 (36) sodium dioctylsulfonsuccinate Example #6 0.3:
  • Table 2 depicts data regarding the reduction in activity and the reduction in polymer produced based on the change observed between the Comparative Example (which did not include an antifouling agent) to each example which included an antifouling additive.
  • Example #1 -3.9% 95.8%
  • Example #2 96.1% 100.0%
  • Example #3 5.3% 92.6%
  • Example #4 8.8% 92.7%
  • Example #5 27.2% 85.7%
  • Example #6 -6.1%
  • Example #8 -0.4% 77.9%
  • Example #9 0.9% 73.0%
  • Example #11 18.9% 89.2%
  • Example #12 -2.2% 73.8%
  • Example #13 -4.4% 84.0%
  • Example #14 11.8% 48.4%
  • a number of antifouling agents suppress polymer formation (for example, at least 5%, 10%, 20%, 30%, 40%, 50%, 60%, 70%, 80%, 90% or even 95% reduction) while not greatly reducing activity (for example, less than or equal to 50%, 40%, 30%, 20%, 10% or even 5% reduction in activity, or even increased activity).
  • any two quantitative values assigned to a property may constitute a range of that property, and all combinations of ranges formed from all stated quantitative values of a given property are contemplated in this disclosure.

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